CN107051219A - The preparation and its application of ionic liquid/graphene oxide gas separation membrane - Google Patents

The preparation and its application of ionic liquid/graphene oxide gas separation membrane Download PDF

Info

Publication number
CN107051219A
CN107051219A CN201710214168.6A CN201710214168A CN107051219A CN 107051219 A CN107051219 A CN 107051219A CN 201710214168 A CN201710214168 A CN 201710214168A CN 107051219 A CN107051219 A CN 107051219A
Authority
CN
China
Prior art keywords
ionic liquid
graphene oxide
gas separation
separation membrane
preparation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201710214168.6A
Other languages
Chinese (zh)
Other versions
CN107051219B (en
Inventor
彭新生
应文
陈丹科
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang University ZJU
Original Assignee
Zhejiang University ZJU
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhejiang University ZJU filed Critical Zhejiang University ZJU
Priority to CN201710214168.6A priority Critical patent/CN107051219B/en
Publication of CN107051219A publication Critical patent/CN107051219A/en
Application granted granted Critical
Publication of CN107051219B publication Critical patent/CN107051219B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B01D53/228Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0079Manufacture of membranes comprising organic and inorganic components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10Supported membranes; Membrane supports
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2

Abstract

The invention discloses a kind of preparation method and applications of ionic liquid/graphene oxide gas separation membrane.Graphene oxide is dispersed among ionic liquid, gas separation membrane is made by vacuum filtration, so that ionic liquid is limited among graphene oxide layer, using ionic liquid to the solubility of gas with various and the difference of diffusion coefficient, the efficient stable separation of gas is realized.

Description

The preparation and its application of ionic liquid/graphene oxide gas separation membrane
Technical field
The present invention relates to the preparation of composite gas separation membranes and application field, and in particular to a kind of ionic liquid/oxidation The preparation and its application of graphene gas separation membrane.
Background technology
Graphene oxide has superior mechanical performance, good chemical stability, unique two-dimensional structure and maturation Preparation technology, multilayer graphene oxide film has nano level passage, there is huge application potential in gas separation field.But Be pure graphene oxide film separative efficiency it is not high, generally require other materials to be modified, prepare laminated film.
Ionic liquid is excellent so that its vapour pressure is small, heat endurance is good, electrochemical window is big etc. as a kind of novel green solvent Gesture is applied to multiple fields.In common gas, ionic liquid is to carbon dioxide compared to there is higher dissolving to other gases Degree so that ionic liquid has the application potential of separation and carbon dioxide-enriched, but due to the characteristic of its liquid, mobility compared with By force so that the less stable in the separation of gas and enrichment process.Ionic liquid is limited in graphene oxide sheet by the present invention In layer, then the problem of solving stability well.
The content of the invention
The present invention is that, in order to overcome pure zirconia graphene film low separation efficiency, and pure ionic liquid continues when being used to separate Property difference defect there is provided a kind of preparation method and applications of ionic liquid/graphene oxide gas separation membrane.
The preparation method of ionic liquid/graphene oxide gas separation membrane, comprises the following steps:By made from chemical oxidation Graphene oxide is dispersed among ionic liquid, obtains graphene oxide/ionic liquid solution;Pass through vacuum filtration again Ionic liquid/graphene oxide gas separation membrane is made by graphene oxide/ionic liquid solution suction filtration to substrate in method.
The technical principle of the present invention is as follows:
The obtained pure zirconia graphene film of vacuum filtration has layer structure of the interlamellar spacing below 1 nanometer;Will oxidation Graphene dispersion is in ionic liquid so that graphene oxide layer and ionic liquid are well-bonded, passes through the side of vacuum filtration Film is made in formula, and ionic liquid is limited among the lamella of graphene oxide;It is oxidized the ion of graphene sheet layer limitation Liquid property can change, the ability of enhancing gas separation, and stability strengthens during gas is separated, Ke Yichang Time is applied.The consumption of regulation ionic liquid and graphene oxide can adjust thickness and the ratio shared by ionic liquid.
Preferably, ionic liquid used be 1- butyl -3- methyl imidazolium tetrafluoroborates, wherein graphene oxide/ The mass percent concentration of graphene oxide is 0.001%~0.02% in ionic liquid solution;Negative pressure during vacuum filtration It is not less than 50KPa;Described substrate is makrolon perforated membrane or inorganic oxide aluminium perforated membrane.
Preferably, ionic liquid used be 1- ethyl-3-methylimidazole tetrafluoroborates, wherein graphene oxide/ The mass percent concentration of graphene oxide is 0.001%~0.02% in ionic liquid solution;Negative pressure during vacuum filtration It is not less than 50KPa;Described substrate is makrolon perforated membrane or inorganic oxide aluminium perforated membrane.
Further, the matter of the ionic liquid described in aforesaid way/graphene oxide gas separation membrane intermediate ion liquid It is 50%~80% to measure percentage.
Ionic liquid made from any of the above-described technical scheme/graphene oxide gas separation membrane, can be used for separating dioxy Change carbon and hydrogen, carbon dioxide and methane.In separation process, applicable pressure is 0.01MPa~0.15MPa, temperature is 20~ 120℃.Either still being directly separated for mixed gas all shows excellent effect from the flux difference of pure gas.
The present invention has the advantages that:Using graphene oxide as support, ionic liquid is limited in graphite oxide In alkene lamella, it greatly strengthen the ionic liquid under the conditions of stability, and confinement and the ability that gas is separated also added By force so that laminated film has significant gas separating capacity.
Brief description of the drawings
Fig. 1 is surface and the profile scanning electron microscopic picture of graphene oxide film;There is obvious elongated sharp fold on surface, Section has obvious layer structure;
Fig. 2 is the surface of [BMIM] [BF4]/graphene oxide gas separation membrane made from embodiment 1 and profile scanning electricity Mirror picture;
Fig. 3 is the surface of [BMIM] [BF4]/graphene oxide gas separation membrane made from embodiment 2 and profile scanning electricity Mirror picture;
Fig. 4 is the surface of [EMIM] [BF4]/graphene oxide gas separation membrane made from embodiment 3 and profile scanning electricity Mirror picture.
Embodiment
Below in conjunction with drawings and examples, the present invention is further illustrated.
Embodiment 1
At room temperature, graphene oxide/[BMIM] [BF that configuration graphene oxide mass percent concentration is 0.016%4] Solution, suction filtration 1ml solution is made on aperture 200nm inorganic oxide aluminium perforated membrane to diameter 25mm under 85KPa negative pressure [BMIM] [BF thick 750nm4]/graphene oxide gas separation membrane, wherein [BMIM] [BF4] mass percent be 56%.From It can see in the electron microscope of film surface, added [BMIM] [BF4] afterwards compared to pure zirconia graphene film, fold is Gentle and reduction;It can see from the electron microscope of section, [BMIM] [BF4] be filled in the lamella of graphene oxide film, Thickness has obvious increase, and interlamellar spacing is stretched, and can't see under Electronic Speculum obvious layer structure.By the seperation film in room The flux of carbon dioxide, hydrogen and methane is measured under the conditions of temperature, 0.06MPa, carbon dioxide and hydrogen, carbon dioxide and first is obtained The flux ratio of alkane is respectively 8 and 30.
Embodiment 2
At room temperature, graphene oxide/[BMIM] [BF that configuration graphene oxide mass percent concentration is 0.004%4] Solution, suction filtration 4ml solution is made 1 μm to diameter 25mm under 85KPa negative pressure on aperture 200nm inorganic oxide aluminium perforated membrane Thick [BMIM] [BF4]/graphene oxide gas separation membrane, wherein [BMIM] [BF4] mass percent be 66%.From film It can see in the electron microscope on surface, [BMIM] [BF4] amount increase so that the fold on surface is further reduced, and is occurred Spherical projection;It can see from the electron microscope of section, film thickness further increases.By the seperation film in room temperature, The flux of carbon dioxide, hydrogen and methane is measured under the conditions of 0.06MPa, carbon dioxide/hydrogen and carbon dioxide/methane ratio is obtained Value is respectively 32 and 382.Under the same conditions carbon dioxide/hydrogen mixed gas and carbon dioxide/first are measured with gas chromatograph The separating property of alkane gaseous mixture, it is respectively 10 and 39 to obtain segregation ratio.
Embodiment 3
At room temperature, graphene oxide/[EMIM] [BF that configuration graphene oxide mass percent concentration is 0.007%4] Solution, suction filtration 2ml solution is made on aperture 200nm inorganic oxide aluminium perforated membrane to diameter 25mm under 85KPa negative pressure [EMIM] [BF thick 800nm4]/graphene oxide gas separation membrane, wherein [EMIM] [BF4] mass percent 58%.From thin It can see in the electron microscope on film surface, added [EMIM] [BF4] afterwards compared to pure zirconia graphene film, fold is flat Relax and reduce;It can see from the electron microscope of section, [EMIM] [BF4] be filled in the lamella of graphene oxide film, film Thickness has obvious increase, and can't see under Electronic Speculum obvious layer structure.By the seperation film under the conditions of room temperature, 0.06MPa The flux of carbon dioxide, hydrogen and methane is measured, it is respectively 9 Hes to obtain carbon dioxide/hydrogen and carbon dioxide/methane ratio 33。
Embodiment described above is a kind of preferably scheme of the present invention, and so it is not intended to limiting the invention.Have The those of ordinary skill for closing technical field, without departing from the spirit and scope of the present invention, can also make various changes Change and modification.Therefore the technical scheme that all modes for taking equivalent substitution or equivalent transformation are obtained, all falls within the guarantor of the present invention In the range of shield.

Claims (7)

1. the preparation method of a kind of ionic liquid/graphene oxide gas separation membrane, it is characterised in that comprise the following steps:Will Graphene oxide is dispersed among ionic liquid made from chemical oxidation, obtains graphene oxide/ionic liquid solution;Again By the method for vacuum filtration by graphene oxide/ionic liquid solution suction filtration to substrate, ionic liquid/graphite oxide is made Alkene gas separation membrane.
2. preparation method according to claim 1, it is characterised in that ionic liquid used is 1- butyl -3- methyl miaows The mass percent concentration of graphene oxide is 0.001% in azoles tetrafluoroborate, wherein graphene oxide/ionic liquid solution ~0.02%;Negative pressure is not less than 50KPa during vacuum filtration;Described substrate is makrolon perforated membrane or inorganic oxide On aluminium perforated membrane.
3. preparation method according to claim 1, it is characterised in that ionic liquid used is 1- ethyl -3- methyl miaows The mass percent concentration of graphene oxide is 0.001% in azoles tetrafluoroborate, wherein graphene oxide/ionic liquid solution ~0.02%;Negative pressure is not less than 50KPa during vacuum filtration;Described substrate is makrolon perforated membrane or inorganic oxide On aluminium perforated membrane.
4. the preparation method according to Claims 2 or 3, it is characterised in that described ionic liquid/graphene oxide gas The mass percent of seperation film intermediate ion liquid is 50%~80%.
5. ionic liquid/graphene oxide gas separation membrane according to made from Claims 1 to 4 any preparation method.
6. the application of ionic liquid/graphene oxide gas separation membrane according to claim 5, it is characterised in that obtained Ionic liquid/graphene oxide gas separation membrane is used to separate carbon dioxide and hydrogen, carbon dioxide and methane.
7. application according to claim 6, it is characterised in that in separation process, applicable pressure for 0.01MPa~ 0.15MPa, temperature is 20~120 DEG C.
CN201710214168.6A 2017-04-01 2017-04-01 Preparation and application of ionic liquid/graphene oxide gas separation membrane Expired - Fee Related CN107051219B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710214168.6A CN107051219B (en) 2017-04-01 2017-04-01 Preparation and application of ionic liquid/graphene oxide gas separation membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710214168.6A CN107051219B (en) 2017-04-01 2017-04-01 Preparation and application of ionic liquid/graphene oxide gas separation membrane

Publications (2)

Publication Number Publication Date
CN107051219A true CN107051219A (en) 2017-08-18
CN107051219B CN107051219B (en) 2020-07-07

Family

ID=59602699

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710214168.6A Expired - Fee Related CN107051219B (en) 2017-04-01 2017-04-01 Preparation and application of ionic liquid/graphene oxide gas separation membrane

Country Status (1)

Country Link
CN (1) CN107051219B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112646613A (en) * 2019-10-12 2021-04-13 中石化南京化工研究院有限公司 Absorbent and method for separating and recovering carbon dioxide in blast furnace gas

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102533406A (en) * 2010-12-23 2012-07-04 中国科学院兰州化学物理研究所 Graphene-containing ionic liquid nanometer composite lubricating membrane
CN103971943A (en) * 2013-01-28 2014-08-06 海洋王照明科技股份有限公司 Preparation method for graphene-ionic liquid composite materials and preparation method for supercapacitor
CN105502350A (en) * 2015-11-29 2016-04-20 南京新月材料科技有限公司 Graphene oxide and ionic liquid composite film and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102533406A (en) * 2010-12-23 2012-07-04 中国科学院兰州化学物理研究所 Graphene-containing ionic liquid nanometer composite lubricating membrane
CN103971943A (en) * 2013-01-28 2014-08-06 海洋王照明科技股份有限公司 Preparation method for graphene-ionic liquid composite materials and preparation method for supercapacitor
CN105502350A (en) * 2015-11-29 2016-04-20 南京新月材料科技有限公司 Graphene oxide and ionic liquid composite film and preparation method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
姜海超: "离子液体性质及其与SO2相互作用机理研究", 《中国博士学位论文全文数据库(工程科技I辑)》 *
赵薇等: "离子液体二氧化碳分离膜研究进展", 《化工进展》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112646613A (en) * 2019-10-12 2021-04-13 中石化南京化工研究院有限公司 Absorbent and method for separating and recovering carbon dioxide in blast furnace gas

Also Published As

Publication number Publication date
CN107051219B (en) 2020-07-07

Similar Documents

Publication Publication Date Title
Joshi et al. Graphene oxide: the new membrane material
Wang et al. Graphitic carbon nitride nanosheets embedded in poly (vinyl alcohol) nanocomposite membranes for ethanol dehydration via pervaporation
Li et al. Laminated self-standing covalent organic framework membrane with uniformly distributed subnanopores for ionic and molecular sieving
Knebel et al. Solution processable metal–organic frameworks for mixed matrix membranes using porous liquids
CN106582317B (en) A kind of preparation method of the metal organic framework modification graphene oxide layer structure composite film for organic solvent nanofiltration
Chen et al. Enhanced gas separation through nanoconfined ionic liquid in laminated MoS2 membrane
Xue et al. A carbon nanotube filled polydimethylsiloxane hybrid membrane for enhanced butanol recovery
Jin et al. High-performance ultrafiltration membranes based on polyethersulfone–graphene oxide composites
Sui et al. The roles of metal-organic frameworks in modulating water permeability of graphene oxide-based carbon membranes
Ma et al. Surfactant-modified graphene oxide membranes with tunable structure for gas separation
CN105502350A (en) Graphene oxide and ionic liquid composite film and preparation method thereof
He et al. Constructing A Janus membrane with extremely asymmetric wettability for water unidirectional permeation and switchable emulsion separation
CN106975370A (en) Ionic liquid/transition metal dichalcogenide gas separation membrane and its application are prepared using capillary effect
CN109621647B (en) Method for separating and enriching carbon dioxide
US9381449B2 (en) Carbon nanotube composite membrane
Ying et al. Laminated mica nanosheets supported ionic liquid membrane for CO2 separation
Han et al. [Cu2 (bdc) 2 (bpy)] n/SPES-C mixed matrix membranes for separation of methanol/methyl tert-butyl ether mixtures
Liu et al. Titanate nanotubes-embedded chitosan nanocomposite membranes with high isopropanol dehydration performance
Deng et al. Oriented arrangement: the origin of versatility for porous graphene materials
Wu et al. Scale-up of zeolite-Y/polyethersulfone substrate for composite membrane fabrication in CO2 separation
CN106902648B (en) Method for preparing ionic liquid/transition metal disulfide gas separation membrane and application thereof
Kreiter et al. Sol–gel routes for microporous zirconia and titania membranes
Hu et al. Improving pervaporation performance of PDMS membranes by interpenetrating polymer network for recovery of bio-butanol
Huang et al. Etching and acidifying graphene oxide membranes to increase gas permeance while retaining molecular sieving ability
León et al. PDMS modified membranes by 1-dodecanol and its effect on ethanol removal by pervaporation

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200707

Termination date: 20210401